Dual phase control



June 10, 1952 T. H. WHALEY, JR

DUAL PHASE CONTROL 4 Sheets-Sheet 1 Filed Nov.

INVENTOR. TVH. WHALEY, JR.

ATTORNEYS June 10, 1952 T. H. WHALEY, JR 2,600,039

DUAL. PHASE CONTROL Filed Nov. 17, 1947 4 Sheets-Sheet 2 A TTORNEVS June 10, 1952 'r. H. WHALEY, JR

DUAL PHASE CONTROL Filed Nov. 1'7, 194'? 4 Sheets-Sheet 5 A T TORNE VS T. H. WHALEY, JR.

June 10, 1952 T. H. WHALEY, JR

DUAL PHASE CONTROL '4 Sheets-Sheet 4 Filed Nov. 17, 1947 INVENTOR.

R v Y E L A H W H T A m w m T T A Patented June 10, 1952 DUAL PHASE CONTROL Thomas H. Whaley, J r., Mount Vernon, N. Y., assignor to Phillips Petroleum Company, a corporation of Delaware Application November 17, 1947, Serial No. 786,441

This invention relates to process control. In one of its more specific aspects it relates to the control of a second liquid phase in processing, wherein the second liquid phase may or may not be desired.

I have devised an apparatus which operates to indicate and/or remove a second liquid phase which floats upon a heavier liquid phase, the second and fighter liquid phase may or may not be desired.

7 Claims. (Cl. 13768) I3. The heavier liquid I2, sometimes termed the kettle or reboiler product in fractionators, may be withdrawn through a pipe I4 controlled by a valve I5 to such disposal as desired. Valve I5 is a motor valve operated by a motor I6. The motor I6 in turn is operated by air, from a source not shown, coming through line 35, through a pilot valve II, through line 34 to the motor I6. Motor I6 then operates the valve I5 through a 10 valve stem linkage 37. The pilot valve I1 is For example, in the extractive distillation of operated by air pressure from line 3| and coming butylene containing stocks with furfural wherein originally from an air supply, not shown, through the butylenes are extracted by or dissolved in the line 25 and control unit 22. Control unit 22 furfural, this mixture settles to the bottom of also controls air from line 25 to pipe 26, which the extraction vessel as a heavy liquid phase. air in turn operates a pilot valve 21. This pilot The remaining hydrocarbons which boil at about valve 21 controls air, originating at a source not the same temperature as the butylenes are inshown, and passing through a line 32 to a pipe tended to distill overhead as vapors from this 33 for operating a motor 28. This motor 28, by extraction column. Conditions exist at times way of alinkage 36, operates a motor valve 29 wherein all of these remaining hydrocarbons are fo control n fluid flowing in line 30. V not distilled overhead and are not dissolved in Within the vessel II is a float I8 adapted to be the furfural, but collect and float as a separate r sponsive o he ei ht of the surface of the liquid layer upon the surface of the furfural or heavier liquid phase I2- I Ca e a lighter liquid furfural-butylene mixture. When such a conphase is also present, this float I8 is intended ti t th operatiun i far from th t deto remain suspended at the interface between the sired. I have devised an apparatus for indicattwo liquid phasese fl 8 i connected by ing and/or removing such a second liquid phase an arm 38 to a tube 20, which in turn extends once it is formed and floats upon the heavier through the wallof the vessel II and terminates liquid phase within the indicator control panel box 22. The 'One'obiect of my invention is to provide a float I9 is intended to float upon the surface of method for process control. Another object of h lighter qu d pha e l3 in e e lighter my invention is to provide a methodfor control liquid phase is P t- T is float I 9 is conof two liquid phases in a process vessel. Still nected by an arm 39 to a shaft 2| which also another object of my invention is to provide a ds t ough the wall of the vessel II and eth for th t l of an d ir d nd terminates in the indicator control panel box 22. liquid phase in a process vessel. Still other ob- A S own in Figure l, the shaft 2 I passes through jects' and advantages will be appreciated by those he cen r of the h ll w t b 0 nd ac or in ly skilled in the art upon reading the following disthe Shaft 2| and u 20 p ss t r u h a common closure and drawing, which respectively describes p ning in the wall of the vessel I I. In this and illustrates the apparatus of my invention. 40 manner only one opening in the wall of vessel II In th drawing, need be provided for accommodating my control Figure 1 shows partly in elevation and partly apparatus. in section one application of my invention. In the bottom of vessel II and within the Figure 2 shows a preferred embodiment of one heavy liquid phase may be a heating coil 23 for portion of my apparatus, partly in section. reboiling purposes, if desired, or an external re- Figure 3 shows one embodiment of the indioiler may be used. cator and control panel. In the upper section of the vessel II is an inlet Figure 4 shows a second embodiment of my p p 24 for mi i hydrocarbon or other feed indicator and control panel. stocks into the vessel II. In a still higher sec- Referring now to the drawing and specifically tion of the vessel II is an inlet pipe 24A through to Figure 1, reference numeral II refers to a which maybe admitted a heavier liquid which column or other vessel containing the liquid ultimately accumulates as the lower liquid phase phases to be controlled. In the bottom of the l2. From the top of the column- II is a pipe 40 vessel is a heavier liquid phase I2 and floating through which distillation vapors may pass to upon that heavier liquid is a lighter liquid phase further processing, as desired.

bearing 41, then within this bearing 41 is placed;

the tube 20. Within the tube 20 is placed another bearing 47A and within this latter bearing is placed the shaft 2|. fit tightly to the sleeve 44, the tube 20 and the shaft 2| in the usual manner, and are adapted to permit easy rotation of the shaft 2| and the;

tube 20. In order to prevent leakage of the contents of the vessel ll, packings 45 maybe provided and inserted as illustrated. The type o f, ;this packing or its method of installation .is immaterial to my apparatus and may be any type of packing orpacking gland which would be suitable fonuse with the apparatus as herein described. Tothe outer end of the sleeve 44-is attached a plate or panel 4| which in one embodiment may be substantially square or rectangular.

in form This plate 4;! is rigidly attached to the sleeve 44 by 'any'method such as welding. To the outer endofthe hollow tube 20 extends through anopening in the plate 4| and is attached :an annular plate 42. This plate 42 is intended to;rotate as tube 28" rotates, rotation being causedby the risingor falling of the heavy- To theouterend 48-01" shaft 2!. is attached a circular plate 43; This plateisiintended to rotateas shaft 2 l rotates; and this rotation in turn is caused by the rising or falling of the light float [9.

Figure 3 is -a detail sketch of a preferred embodiment ofthe indicating and control apparatus which is mounted on the panel plate 4|. end- 48-,(of the shaft 2|) is rigidly attached an arm Thisarm it extends downward some distance and terminates in a pointer whichis intended -to;point to numerals on a scale 54.

To the-outer end of the. tub'e20, as mentioned hereinbefore, isattachedthe annular plate 42 and to thisannular plate 42 is attached a member 52. This member 52 accordinglyv rotates around the center-of the shaft, 2| butin accordance with the; movements of the hollow tube 20. The lower endof this member 52 terminates as a pointer 64 for indicating plus or minus values on the scale 55;, Scale 55;-is attached directly to the panel plateg M- To the member 52. is. rigidly attached a controller mechanism '52 which may consist of a T-tube-orifice-bafiie assembly. One armof the T'- receives air from a source, not shown, and the air -passes through an orifice 63, and through a second orifice 6B, pressure being communicated through the leg of the T Gltothe motor of a valve. to becontrolled. The lower portion of the arm 5|,has a threadedopeningfor accommoda- These bearings, of course,

To the j and associated parts and with a scale; 87.

pivoted at 68 to the panel plate M, as shown. This arm 61 is provided with a threaded opening for accommodation of a bolt or screw member 89, one end of which has a bolt head for adjustment purposes and the other end terminates adjacent a baffle member 10. This baflle member 10 is pivoted at ll to the panel plate 4 I. One end of the baffle member'l'il is held tightly against the 'end of the screw 69 by a tension spring I2. The other end of the baffle 18 is positioned in operating relation to an orifice which is a part of a T member 13, similar to the T member 62. This T member 73 is composed of a tube leading from an air, supply, the orifice T6, the orifice l5 andtthe tube 14. This latter tube leads to and communicates pressure to the motor of the motor valve to be controlled. The T member 13 is attached'to the panel plate by attachment TI.

. The controller mechanisms 62 and T3 are shown herein as T-tube-orifice-baiile assemblies, but are not so. limited since any suitable conventional controller .mechanism may be used.

Figure i is somewhat similar to Figure 3 but showsanother embodiment of the control end indicating portion of my apparatus. This embodiment contains the same base plate M as in Figure 3; To this base plate is-attached the member 52 the linkage 65, 6-7, and the battle apparatus consisting of the battle member Iii and the T member 13 and associated parts. The member 52, as inFigure 3, is attached to the annular ring 42 and is accentuated by the rising and falling of the heavy float l8. This member 52 is provided.

with a nozzlemember 62, the baffle member 51 The member 52 terminates at point 64 as an indicator along scale 55. One end of the arm 82 is attached at a pivot 81 to one end of the light liquid float shaft and at theother end through pivot 83; to an arm 84-. Arm 84 has a slot 85 for accommodationiof the guide pin 86. Belowthe guidepin 86; the arm 84 terminates as a pointerpointingto the scale 8-! on the member 52. Above tended .thatas the heavy float i8 rises above a predetermined level the heavy liquid material in the bottom of the vessel H will-be withdrawn through pipe! has controlledby valve I5 until the level of this liquid reaches. the predetermined value. This. operation may be explained as follows, briefly; by-reference to Figure 1, float I 8 rises (also see Figure 2) to opierate the control box 22 which in turn controls air pressure in line 3| and operates pilot valve 1 'Lwhich in turn-permits passage .ofair from pipe: 35 through pipe 34 tothe motonfli; Thismotor lfi then opens valve I5 which operation permits passage of the heavy phaseil2through line 14 to such disposal as de 1 sired; When the level of the heavy liquid phase I2 *decreasesito a certain position, the-fio'at-lfi These flexible connecthen drops to reverse this operation and valve I5 closes. g A

In detail; this operation with control panels of Figures 3 and 4 is as follows: When heavy fluid I8 rises the' tube 20 rotates clockwise, as does base member 52: Upon thi rotation of base member 52,-linkage arm 65 moves toward the right as does the upper end of arm 61. This movement of arm 61 around its pivot 68 as the center moves screw 69 toward the right and this movement moves baiiie I0 around pivot point H so that air flowing through bleed nozzle is closed off or partly closed off. The closing off of the air flowing from bleed nozzl I5 raises the pressure of the air in tube I4 and since tube I4 connects with tube 3|,

this increase in air pressure is communicated to the top :of the pilot valve IT. This increase in pressure opens the pilot valve I! to permit flow of .air from pipe 35 throughv pipe 34 to the motor I6 and motor I6 accordingly opens the motor valve I5. When motor valve I5 opens, then the lower liquid phase I5 passes out through pipe I4. As the level of the heavy liquid I2 drops, the heavy float I8 drops also and the dropping of float I8 rotates the tube anti-clockwise, which rotation reverses the movement of the linkage arms 65 and 51 to. move the bafile I0 farther away from the bleed-nozzle I5. Thus, the opening of nozzle I5 permits'air to flow therethrough and causes a decrease of pressure in the tube 14. Andas mentionedabove, since tube I4 is connected with tube 3|, pressur in 3| decreases to permit closing of the pilot valve I1 and. accordingly this shuts off the-air from pipe 35 to pipe 34. Decrease of pressure-in pipe 34 then permits motor IE to close the motor valve I5.

. When some lighter liquid I3 accumulates upon th surface of the heavier liquid I2, float I8 still rides upon the surface of the heavier liquid I2 while the lighter float I9 rises with the surface of the lighter liquid.

Briefly, according to the embodiment of Figure 3, asthelight liquid phase I3 increases in volume in the vessel I, the light float I9 rises and rotates the shaft 2| in a clockwise direction. This clockwise rotation of shaft 2| rotates the arm 5| in a clockwise direction around point 48 to move screw 56 toward the left and close th bleed nozzle 60. Air pressure in the tube. 6| increases and this pressure increase is communicated to tube 26 (Figure 1) to operate pilot valve 21 and. motor 28 and finally to open the motor valve 29. When the liquid. level of the lighter phase I3 drops the lighter float I9 drops to reverse the operational steps and accordingly the motor 29 is closed.

' In more detail, as float I9 rises, and still according to the embodiment of apparatus of Figure 3, the. end 48 of shaft 2| rotates in the clockwise direction. This rotation moves arm 5| also in a clockwise rotation around point 48 as the center. The pointer on the lower end of arm 5| also moves toward the left. This movement moves screw 56 to force the bafile 5'! against the bleed nozzle 60 whichoperation causes the building up of air pressure in the tube 6| and since outlet tube 6| is connected directly with tube 26 of Figure 1, this pressure is communicated through tube 26 to the pilot-valve 27. Pilot valve 21 opens to admit air from pipe 32 through pipe 33 to operate the motor 28. Motor 28 accordingly opens the motor valve 29 to permit flow of control fluid through pipe 30. This fluid in pipe may be steam, for example it may be steam for furnishing reboiling heat in reboiler'coil 23 in the base of the column II. The additionof heat to this reboiler will then raise thetemperat'ur of the heavier liquid: I2 and in turn will cause thelighter liquid I3 to boil away or vaporizer As the lighterliquid I3 disappears as vapor, of course, its liquid level will dropand as the level drops the float I9 drops also to reverse the control steps just mentioned. Reversing of these control steps cause motor valve 29 to close, thereby shutting ofi the steam in pipe 30 from flowing to the reboiler coil 23.

Thus, in this operation it is seen that asithe level of the heavier liquid I2 rises, the member 52 rotates to operate through linkages B5 and B1, to operate the motor valve I5, and this operation is independent of the height of the level of the lighter liquid I3. This operation will be the same whether there is or is not any lighter liquid present. In like mannenwhen the lighter liquid I3 is present'the float' I9 operates through shaft 2| to move arm 5| to close the bleed nozzle 69 which, as mentioned, will promote'removal of the light liquid l3. All this operation is independent of the position of the-level of the heavier liquid. When the level of the heavier liquid drops, the level of the lighter liquid also drops but the volume of the lighter liquid remains the same. When the heavier liquid level drops, the float I8 and the float I9 both drop exactly the same amount and the member 52 and the arm 5| both rotate in a counterclockwise direction and the position of the baflie 51 with respect to the bleed nozzle 60 is not altered in any manner. And in like manner, when the level of the heavier liquid rises both floats I8 and I9 rise in equal amount and cause rotation of the member 52 and arm 5| in a clockwise direction and accordingly the baffle member 51 is not moved with respect to the end of the bleed nozzle 60. The only control which operates when these latter conditions exist is the baiile member I0 with respect to the bleed nozzle I5 and this operation, of course, as mentioned before, controls the level of the heavier liquid.

When the lighter liquid I9 increases in volume, the float I9 rises without imparting any move ment whatever to the heavier float I8 andthe rising of float I9 causes movement of the arm 5| and thereby movement of the baffle 51 with respect to the bleed nozzle 6|] without in any manner causing movement of member 52, linkages 65 and 61 and baflie III with respect to bleed nozzle I5.

Thus, it will be seen thatthe volume of heavier liquid in the bottom of column II may be controlled quite independent of the lighter liquid riding on its surface and in like manner'the volume of the lighter liquid I3 can be controlled without in any manner affecting the volume of the heavier liquid under it.

Referring to the apparatus of Figure 4 for an embodiment based upon the relative positions of the shaft 2| and the tube 20 in the sidewall of the vessel II, in which case the tube 20need not be a tube but may bea shaft exactly like shaft 2|. In fact, I prefer that this member be a shaft because it is smaller in diameter, is more easily packed, and the operation of the float is less afiected by friction. Thus for the embodiment of Figure 4 there will need be two openings or one large opening in the wall of vessel I I large enough to pass the two shafts and the two floats. Both shafts may terminate in points similar to point 48 of Figure 3 and this point is also shown in Figure 4. Reference numeral 48A of Figure 4 refers to the end of the shaft upon which is mounted the heavier float while point 8| refers to the end of the shaft upon the operation of theracoparatusrof migrate.

-51. closer to the bleed 'nozzle iliflwvhie .will-acause an. increase-of air; p ssure-in. 11 32.8 l and the-effect of:this .incr.ease of; pressureiilrtllbe amaz which is mounted .-.the;lighter.: float escrow 156 :then vis.:moved :to' the or ztozthe". left :hy

movement of anarmsSdZ-nhich inturnlisrrnovcli by anxarm. 82 through: the ipivotr point ,83.

82 ;is rotated :by the sshait :terminated: atmo ni lighter liquid rises the armzBkrotates in azeloc W186 direction and thismotation ;in turnemoves arm :84 toward .the left. ;.'his:-mot men hashes screw .56 toward the left-andziimve lie-333 313 overn nt .6 L has been ;,explainedrhereinheiore- Whenthe level of: thellighter. liqu d-sirens. QflQart l9 -;wi1l 111101 and this .w ll ea eemovem n o the arm-8.21111 a c unterclo kwise; d rect on. which v men will m ve th v afiie 1 f rth away from .thelbleedno zle fill ,d'r hi movem nt il cause-a -..d c.r.eas impreesure; n ribe 5 v and .th results of th s dmprinnressure:havetalso been explained.

Thus, in su n up the op ration :9? t e apparatuso i u e awhen th i uriee 0f t heavier liquid rises thesurfeoe "of th li ter liquid rises a a d he-on y b e .11 Q erate .isJfl and thiswill op rate os ee memo i of some .of the heavie i id.- W en -the li hte float 19 moves, float,l-8 .vvill not moveonfiqonly arms82 and will moveto operate bleed-nozzle .60. 'Thus the volume-of thelighter liquidrnay be controlled independentlyotthevolurne ,ofthe heavier liquid in vessel; I l.

The operation of the lighter. float l9 hasgbeen explained for controlling .stea-msin. 1 ine-.-3 0 .and furnishing reboilingheat .tothe reboilencoil 23. Float 1.9 may :oontroLother operational ,steps relative to vessel II, as for example, furfural feed through line 24a, or hydrocarbon feedstock containing butyleneand other hydrocarbons con.- taining four carbon atoms per molecule-through the feed line 24. Since thefurfuralis heavier than the hydrocarbon feed,.thefurilural will flow l r downward in the column. dissolving the hutylene in pre ference to the other hydrocarbons. .I L-this particular case the temperature of-thacolumn is intended to be such that the undissolved hydrofiarbons will distill and rise .upward ..and flow in countercurrentrclation tothe iurfural and finally .leave the tower through the overhead pipe (50. When theoperation .isnormal, onlyaa heavy i liquid consisting of -furfural .and. .d fifiolved hydrocarbons, mainly ,butylene. will heJin the bottom of the vessel and the other. hydrocarbons will rise as vapors and leave the tower-through pipe itfl. Conditions may. occur wherein all otthe hydrocarbons to be vaporized will not hegnaporized and these. may then accumulate ,onthelSutf-ade o the f-urfural as. a separ teand light liquid hase since these other hydrocarbons "are-Jess soluble than butylenein furfural- When.this...chn it m exists, corrective steps should betglgen tpjremgve thisl eht rliqu dphaseelig terlinu drhase may be removed by adding rebelling heat through coil'23 as mentioned before, or the liquid may be dumped in a manner similar to the removal of the heavier liquid 1'2. In this case, the motor 28 will operate the valve'29' and perrnit fiowpf the lighter liquid 13 through the linefidto-sorne desired disposal. Then when-the'float'lfi indicates that all or substantiallyall of the'light liquid His gone, the valve "29 w-ill-close. I

This light liquid phase mayalso -be eontrolled iii eby. controlling .the .volume .of hydrocarbon :icetl added to the vessel H for processing. elifasome flight. ,liquid accumulates on the .isurface got .the heavier :liquid, this step would: indicate thatimo much iced is .being :passed rtro the J column-123ml valve 19 amayibe installed in feedline 245mm 1 the; float. 9- rises the 1 valve 121 may; themclosepfi a .portlon of .t-he :feed to the column ta constant heatinput, :say. by :reboiler; .doilzli. flThe .volumenaf the ;-lighter liquid Lwill .rlecrease by .vaporizi-ng and the. vapors; passing; upward. inzthe tower and.-.o.ut;.the-v pipe 40.

.Jln .eanother manner the-.volumelcr li hter through ifeed .pipe 2-4. Y :Ingthis manner..:.as:the

.fioatl t9 rises the motor-valve ;29.;may: beoneratcd topenmitrnassage oi steamor other. heatingagent through. pipejfl to. a; heat. =.exchaneeriinserted feed 19196, 24. {thus when; the hydrocarbonriecd entering the itowerd I :through pipe. isrheatcd more hydrocarbons V will. be and rless re-.- rnain as liquid,.the1 level ofzthe iightenliquidewizll notincreasenoriyvill decrease untilitsfioat oner: :ates to :close. off the. heat to: tha'feem line.

The volume v of the lighter liquidz l3imaysiure that he .c ntrollerl in ravmanner-similarziogthat just. described by. controlling. the. volume off-fur. fural. entering through: 1ine324-A, or-by-contnolling its temperature,. or. other variables.

In 1 some cases in .which :a :large numhertpof traysis-required; to; make .argiven separation-for example 10.0. trays and- 8111683115 isenotord-inarily practical to construct asa singlavessel-azlfldttay column, such a'fmctionatonmavbe mazdeinetwo or more units. The bottoms.from-..the.tep=aunit in thiscase will he .addedto theitop ofatheibottom unitasthe liquid reflux :andveipors strum the top. of this: hottomuunit Will be. passediintothe bottom of the top unit. Underisome condltions the kettle of the top unit may;-be'.the.-,-point-- at which a. second liquidvphasesmayeappearewhile rehoil heat is of-course addedtotheikettle' of the'hottom. section. Irr.this. case-m'y dual control apparatus may. be. installed-1'i-nztheiloweraportion of the; top sectionwhile the -reboilen ooiI mayabe placed-in theikettle ofthelower-section. aAsniene tioned. herein 'my rlual control apparatusamay be adapted tocontrol reflux tofthert'op ofathe' top section, or .to: controlany. other process-l point dee sired. In Figure 1'. ofcthe; drawing a single :ues'sel fractionator is. shown for. purposes 0t simplicity.

If desired, the. .air nozzle-assembly ifl of fig ures :3. and. 4-. may.- he. placed -.on= the? opposite-side of theabafiie .57 .so that movement of the adiusb ahle. 1.sc-reiv .153 tram; right to .leitlmll pe zth nozzle; in place ofhclosing nozzle as -shownl suchhafilesiare usually mademtssprin'g steel so that if:they touch or exert--pressureagainst thp oisificezafifi, the battle-will-bend'ahd will not'damagethe orifice-or any other-part-ofi the-apparatus; Thesarne holds for' the bafile-assemblyemergures -3 and 4 that 1 the ain nozzle 13 main: placed on the- -oppo siteside-of thehafile ifl.

In cases in which the embodiment of Figure '4; is usedthat is, the two' float shafts are esarareafrom one another, theseshafts: and{ a lgih fggl semblies maybe replaced-byterque; mas ges blies whichare-k-nownirrtheart.

' '-lVLy rnethodof eentrohef this two phase-condi-; tion-wi-ll -ha'veapplication in any 'processjyviierein a second and undesired liguicl phase of-lov rer,

specific gravity may accumulate upon the sur face ofa liquid-phase-ofhigher spepijic gravity and it is not li-mi-tedto the example herein iven? While I have shown air pressure means'for'opcrating my -control system I do" not wish to be limitedthereby since electrically operated-apparatus mayalso be used. Such electrically operated apparatus is known in the art. v The apparatus may be constructed of conventional materials such as are available on the market. 1 If corrosive materials are being processed, of course, structural material should be selected accordingly. K I 7 It will be obvious to those skilled in the art that many'variations in my method of control and in the apparatus form may be made and yet remain within the intended spirit and scope of my invention. I do notwish to be limited by the example discussed but only by the appended claims. 1

Having disclosed my invention, I claim:

1. A dual liquid level responsive device for indicating the levels of two liquid phases wherein oneliquid is of low specific gravity and floats upon the surface of the second liquid of high specific gravity, comprising in combination a first float for floating on the surface of said low specific gravity liquid, a second float for floating on the surface of said high specific gravity liquid, a

first arm and shaft for converting vertical movements of said first float to rotary movements, a second arm and shaft for converting vertical movements of said second float to rotary movements, a first indicator attached to said second shaft and disposed to rotate therewith, a second indicator attached to said first shaft and disposed to rotate therewith and to rotate relative to said first indicator, said first indicator being for indicating the level of said second liquid and said second indicator being for indicating the level of said first liquid with respect to the level of said second liquid.

2. A dual liquid level responsive device for indicating and controlling the levels of two immiscible liquids wherein one liquid is of low specific gravity and floats upon the surface of the second liquid of high specific gravity, comprising in combination a first float for floating on the surface of said low gravity liquid, a second float for floating on the surface of said high specific gravity liquid, a first arm and shaft for converting vertical movements of said first float to rotary movements, a second arm and shaft for converting vertical movements of said second float to rotary movements, a first indicator and control member attached to said second shaft and disposed to operate therewith, a second indicator and control member attached to said first shaft and disposed to operate therewith and to operate relative to said first indicator and control member, said first indicator and control member being for indicating and controlling the level of said second liquid and said second indicator and control member being for indicating and controlling the level of said first liquid with respect to the level of said second liquid.

3. A dual liquid level responsive device for controlling the levels of two immiscible liquids wherein one liquid is of low specific gravity and floats upon the surface of the second liquid of high specific gravity, comprising in combination a first float for floating on the surface of said low gravity liquid, a second float for floating on the surface of said high specific gravity liquid, a first arm and shaft for converting vertical movements of said first float to rotary movements, a second arm and shaft for converting vertical movements of said second float to rotary movements, at first control member attachedto said second shaft and disposed to operate therewith, a second control member attached to said first shaft and disposed to operate therewith and to operate relative to said-first control member, said first control member being for controlling the level of said second liquid and said second control member being for controlling the level of said first liquid with re spect to the level of said second liquid. a

4. A dual liquid level responsive device for indicating the levels of two liquid phase wherein one liquid is of low specific gravity and floats upon the surface of the second liquid of high specific gravity, comprising in combination a first float for floating on the surface of said low specific gravity liquid, a second float for floating on the surface of said high specific gravity liquid, a first arm and shaft for converting vertical movements of said first float to rotary movements, a second arm and shaft for converting vertical'movements of'said second float to rotary movements, a first indicator member attached to said second shaft and disposed to rotate therewith, a second indicator member attached to said first shaft and disposed to rotate therewith and to move relative to said first indicator member, said first indicator member indicating the level of said second liquid and said second indicator member indicating the level of said first liquid with respect to the level of said second liquid.

5. A dual liquid level responsive device for indicating and controlling the levels of two liquid phases wherein one liquid is of low specific gravity and floats upon the surface of the second liquid of high specific gravity, comprising in combination a first float for floating on the surface of said low specific gravity liquid, 2. second float for floating on the surface of said high specific gravity liquid, a first arm and shaft for converting vertical movements of said first float to rotary movements, a second arm and shaft for converting vertical movements of said second float to rotary movements, a first indicator member attached to said second shaft and disposed to rotate therewith, a second indicator member attached to said first shaft and disposed to rotate therewith and to move relative to said first indicator member, a first control member attached to said first indicator member and disposed to operate therewith, said first indicator member indicating the level of said second liquid and said second indicator member indicating the level of 'said first liquid with respect to the level of said second liquid, a second control member attached to said second indicator member and to said first indicator member and disposed to operate therewith.

6. A dual liquid level responsive device for indicating the levels of two liquid phases wherein one liquid is of low specific gravity and floats upon the surface of the second liquid of high specific gravity, comprising in combination a first float for floating on the surface of said low specific gravity liquid, a second float for floatin on the surface of said high specific gravity liquid, a first arm and shaft for converting vertical movements of said first float to rotary movements, a second arm and shaft for converting vertical movements of said second float to rotary movements, a first indicator member attached to said second shaft and disposed to rotate therewith, a second indicator member comprising a lever arm secured to said first shaft and disposed to rotate therewith and a link member pivoted to said lever arm and having a lost motion .slidmgcennectie wi hse lifi semdicemrwh lwi-filae msttienofiyea-idj-n dicatm:' indic .thfillfiye iili said: seeend: 'liewd and th 61m :pneitien .Qf eazida link membeit amtea-idy firstfind-ieaten member: indicates. the lev l 0fiqwith. respccibto; the'llevel'ofi; said secomk liquid;

.7. Acduah liquid leezelgrespenslve deviceficmmdieating and; cum-rolling; :the Jewels; of -=twcr liquid phases Whe1Z&iI1. .OIl6i liquid, 1820f; law-specific g'mvity and; :fieaitsa upczmthe surface of the secend highspecifieg'mvity, COmIJIiSiUgflW OOHI- hinailion; a first-float fer-floating on the surface of; specific' grawlty liquid; a second float in! fl at g: on the eminent saidhigh .specific .ventical mevements of. saidfirst. float 420x1 0.- 1any.movements, a secondiarmand? :shaffii. for cenvertingt vertical movements: of said eecend flnatltomorary mnvementea first. indicatetmembenattachect ta .said secondshaft; and, dispgsed 110;101582138 '.therewith,;a1:finst: control; member at: tached: tn said first indicaztor-smcxnbcniamh dispflsedi t0 .operatei theremim m second. indicator c 1:2 member a. lever arm secm'fldi mimid firsfi skafit; and disposal meretevtael'ilaaewv iilziz"122ml a; link-member" :pizvctefiom -sel'd 1am: having-a: lest merion sliding. mnneetm withlsaid first indicater whereby the nosi'tien-etsaidzgflrst indicator indicatesw the level-0i; saidesecomeliqmld and the relative :DOSitziOH-Ofsaid linkmember and saidlfirstz-mdicatonmembenindicatesrithe levelsei said. first-liquid with respect to; the. leveL-ot'saldsecond liquid; and a second commlzmbemafi flashed: to; said; -member am to said, first indicate: member and. dispesedx to? cperat e-fihemwith 'BHQMAS JR:

REFERENCES: CLTED' The following references are of recorddmflre file of fizhis: patent;

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